GB1136940A - Catalysts - Google Patents
CatalystsInfo
- Publication number
- GB1136940A GB1136940A GB25832/66A GB2583266A GB1136940A GB 1136940 A GB1136940 A GB 1136940A GB 25832/66 A GB25832/66 A GB 25832/66A GB 2583266 A GB2583266 A GB 2583266A GB 1136940 A GB1136940 A GB 1136940A
- Authority
- GB
- United Kingdom
- Prior art keywords
- oil
- june
- heavy
- distillates
- light
- Prior art date
- Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
- Expired
Links
- 239000003054 catalyst Substances 0.000 title abstract 2
- 239000003921 oil Substances 0.000 abstract 5
- IJGRMHOSHXDMSA-UHFFFAOYSA-N Atomic nitrogen Chemical compound N#N IJGRMHOSHXDMSA-UHFFFAOYSA-N 0.000 abstract 4
- PXHVJJICTQNCMI-UHFFFAOYSA-N Nickel Chemical compound [Ni] PXHVJJICTQNCMI-UHFFFAOYSA-N 0.000 abstract 2
- 239000007789 gas Substances 0.000 abstract 2
- 229910052500 inorganic mineral Inorganic materials 0.000 abstract 2
- 239000011707 mineral Substances 0.000 abstract 2
- 229910052757 nitrogen Inorganic materials 0.000 abstract 2
- 239000004215 Carbon black (E152) Substances 0.000 abstract 1
- UFHFLCQGNIYNRP-UHFFFAOYSA-N Hydrogen Chemical compound [H][H] UFHFLCQGNIYNRP-UHFFFAOYSA-N 0.000 abstract 1
- ZOKXTWBITQBERF-UHFFFAOYSA-N Molybdenum Chemical compound [Mo] ZOKXTWBITQBERF-UHFFFAOYSA-N 0.000 abstract 1
- PNEYBMLMFCGWSK-UHFFFAOYSA-N aluminium oxide Inorganic materials [O-2].[O-2].[O-2].[Al+3].[Al+3] PNEYBMLMFCGWSK-UHFFFAOYSA-N 0.000 abstract 1
- 238000006243 chemical reaction Methods 0.000 abstract 1
- 238000001125 extrusion Methods 0.000 abstract 1
- 229930195733 hydrocarbon Natural products 0.000 abstract 1
- 150000002430 hydrocarbons Chemical class 0.000 abstract 1
- 239000001257 hydrogen Substances 0.000 abstract 1
- 229910052739 hydrogen Inorganic materials 0.000 abstract 1
- 238000005984 hydrogenation reaction Methods 0.000 abstract 1
- 229910052751 metal Inorganic materials 0.000 abstract 1
- 239000002184 metal Substances 0.000 abstract 1
- 239000000203 mixture Substances 0.000 abstract 1
- 229910052750 molybdenum Inorganic materials 0.000 abstract 1
- 239000011733 molybdenum Substances 0.000 abstract 1
- 229910052759 nickel Inorganic materials 0.000 abstract 1
- 239000002245 particle Substances 0.000 abstract 1
- 239000003079 shale oil Substances 0.000 abstract 1
- 239000000126 substance Substances 0.000 abstract 1
- 239000000758 substrate Substances 0.000 abstract 1
Classifications
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01J—CHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
- B01J21/00—Catalysts comprising the elements, oxides, or hydroxides of magnesium, boron, aluminium, carbon, silicon, titanium, zirconium, or hafnium
- B01J21/02—Boron or aluminium; Oxides or hydroxides thereof
- B01J21/04—Alumina
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01J—CHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
- B01J23/00—Catalysts comprising metals or metal oxides or hydroxides, not provided for in group B01J21/00
- B01J23/70—Catalysts comprising metals or metal oxides or hydroxides, not provided for in group B01J21/00 of the iron group metals or copper
- B01J23/76—Catalysts comprising metals or metal oxides or hydroxides, not provided for in group B01J21/00 of the iron group metals or copper combined with metals, oxides or hydroxides provided for in groups B01J23/02 - B01J23/36
- B01J23/84—Catalysts comprising metals or metal oxides or hydroxides, not provided for in group B01J21/00 of the iron group metals or copper combined with metals, oxides or hydroxides provided for in groups B01J23/02 - B01J23/36 with arsenic, antimony, bismuth, vanadium, niobium, tantalum, polonium, chromium, molybdenum, tungsten, manganese, technetium or rhenium
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01J—CHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
- B01J23/00—Catalysts comprising metals or metal oxides or hydroxides, not provided for in group B01J21/00
- B01J23/70—Catalysts comprising metals or metal oxides or hydroxides, not provided for in group B01J21/00 of the iron group metals or copper
- B01J23/76—Catalysts comprising metals or metal oxides or hydroxides, not provided for in group B01J21/00 of the iron group metals or copper combined with metals, oxides or hydroxides provided for in groups B01J23/02 - B01J23/36
- B01J23/84—Catalysts comprising metals or metal oxides or hydroxides, not provided for in group B01J21/00 of the iron group metals or copper combined with metals, oxides or hydroxides provided for in groups B01J23/02 - B01J23/36 with arsenic, antimony, bismuth, vanadium, niobium, tantalum, polonium, chromium, molybdenum, tungsten, manganese, technetium or rhenium
- B01J23/85—Chromium, molybdenum or tungsten
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01J—CHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
- B01J35/00—Catalysts, in general, characterised by their form or physical properties
- B01J35/40—Catalysts, in general, characterised by their form or physical properties characterised by dimensions, e.g. grain size
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01J—CHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
- B01J35/00—Catalysts, in general, characterised by their form or physical properties
- B01J35/60—Catalysts, in general, characterised by their form or physical properties characterised by their surface properties or porosity
- B01J35/64—Pore diameter
- B01J35/651—50-500 nm
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01J—CHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
- B01J35/00—Catalysts, in general, characterised by their form or physical properties
- B01J35/60—Catalysts, in general, characterised by their form or physical properties characterised by their surface properties or porosity
- B01J35/66—Pore distribution
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01J—CHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
- B01J37/00—Processes, in general, for preparing catalysts; Processes, in general, for activation of catalysts
- B01J37/0009—Use of binding agents; Moulding; Pressing; Powdering; Granulating; Addition of materials ameliorating the mechanical properties of the product catalyst
Landscapes
- Chemical & Material Sciences (AREA)
- Engineering & Computer Science (AREA)
- Materials Engineering (AREA)
- Organic Chemistry (AREA)
- Chemical Kinetics & Catalysis (AREA)
- Catalysts (AREA)
- Production Of Liquid Hydrocarbon Mixture For Refining Petroleum (AREA)
Abstract
1,136,940. Hydrotreating. ENGLEHARD MINERALS & CHEMICALS CORP. 9 June, 1966 [11 June, 1965], No. 25832/66. Heading C5E. [Also in Division B1] A mineral hydrocarbon containing nitrogen, for example a light cycle oil, a heavy cycle oil or a heavy gas oil is hydrogenated at a temperature of from 550 to 900 F. using a presulphided catalyst comprising 0À05 to 40 wt. per cent hydrogenation metal from Groups VB, VI B and/or VIII, for example molybdenum and nickel on a substrate made by extrusion of a mixture of alumina which is substantially free of particles of more than 30 microns in size. Feeds generally mentioned are naphthas, kerosenes, straight run and cracked distillates, distillates from shale oil or gilsonite deposits, light and heavy cycle oils, gas oils, and may contain up to 3% nitrogen. Reaction conditions are: pressure 200 to 3000 p.s.i.g., W.H.S.V. 1 to 8, amount of hydrogen 500 to 5000 S.C.F/B.
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
US463393A US3361682A (en) | 1965-06-11 | 1965-06-11 | Alumina-based catalyst and method of preparing same |
Publications (1)
Publication Number | Publication Date |
---|---|
GB1136940A true GB1136940A (en) | 1968-12-18 |
Family
ID=23839924
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
GB25832/66A Expired GB1136940A (en) | 1965-06-11 | 1966-06-09 | Catalysts |
Country Status (4)
Country | Link |
---|---|
US (1) | US3361682A (en) |
JP (1) | JPS5128592B1 (en) |
GB (1) | GB1136940A (en) |
NL (1) | NL6608097A (en) |
Families Citing this family (11)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US3526602A (en) * | 1968-02-09 | 1970-09-01 | Shikishima Mui Bii Kk | Catalyst carrier and process of making the same |
US3674680A (en) * | 1970-03-09 | 1972-07-04 | Standard Oil Co | Process and catalyst for hydroprocessing a resid hydrocarbon |
JPS5022992B1 (en) * | 1970-05-29 | 1975-08-04 | ||
US3883307A (en) * | 1971-10-21 | 1975-05-13 | Ambac Ind | Gas analyzer resistance element |
US3856708A (en) * | 1972-04-10 | 1974-12-24 | Reynolds Metals Co | Alumina catalyst support |
US3876680A (en) * | 1972-07-14 | 1975-04-08 | Gulf Research Development Co | Catalyst for the hydrogenation of aromatics |
US3959520A (en) * | 1974-10-21 | 1976-05-25 | Universal Oil Products Company | Continuous system for providing a catalytic coating on support members |
US4447556A (en) * | 1983-04-04 | 1984-05-08 | Uop Inc. | Hydrocarbon conversion catalyst and use thereof |
US6962684B2 (en) * | 2001-05-31 | 2005-11-08 | Sumitomo Chemical Company, Limited | Activated alumina formed body and method for producing the same |
US7560412B2 (en) * | 2004-08-14 | 2009-07-14 | Sud-Chemie Inc. | Fluid/slurry bed cobalt-alumina catalyst made by compounding and spray drying |
FR2910353B1 (en) * | 2006-12-21 | 2009-03-06 | Inst Francais Du Petrole | PROCESS FOR HYDROCONVERSION IN SLURRY OF HEAVY HYDROCARBON LOADS IN THE PRESENCE OF A DISPERSE ACTIVE PHASE AND AN ALUMINUM OXIDE |
Family Cites Families (2)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US3267025A (en) * | 1961-05-22 | 1966-08-16 | Sinclair Refining Co | Catalytic hydrocarbon conversion process |
US3193348A (en) * | 1962-02-19 | 1965-07-06 | Sinclair Research Inc | Method of producing boehmite having crystal size in excess of 100 a |
-
1965
- 1965-06-11 US US463393A patent/US3361682A/en not_active Expired - Lifetime
-
1966
- 1966-06-09 GB GB25832/66A patent/GB1136940A/en not_active Expired
- 1966-06-10 JP JP41037140A patent/JPS5128592B1/ja active Pending
- 1966-06-10 NL NL6608097A patent/NL6608097A/xx unknown
Also Published As
Publication number | Publication date |
---|---|
DE1542118A1 (en) | 1970-03-26 |
US3361682A (en) | 1968-01-02 |
JPS5128592B1 (en) | 1976-08-20 |
DE1542118B2 (en) | 1975-06-19 |
NL6608097A (en) | 1966-12-12 |
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